Process for treating contaminated soil

ABSTRACT

A process for the purification of soil contaminated with organic material is provided. The preferred process generally involves superposed attrition and classification processes, which lead to removal and concentration of highly contaminated fractions. The process may also include a step of flotation whereby hydrophobic materials in the soil are released to an interface with air bubbles, and are floated to the top of a flotation cell. In preferred processes according to the present invention, soil to be treated is extracted from a contaminated site, and is broken into relatively small particles. These particles are preferably treated in attrition and classification steps, to remove fine, slow settling contaminated materials such as wood and fine soil materials. The resulting isolated coarser materials are then treated by flotation for a final polishing step. The process is particularly well adapted for use in treating soils contaminated with oil and grease materials containing PCP therein, from wood treatment plants or the like.

The present application is a Continuation-In-Part of U.S. applicationSer. No. 07/388,748, filed Aug. 2, 1989, and issued as U.S. Pat. No.4,923,125 on May 8, 1990, which was a Continuation of application Ser.No. 07/153,240, filed Feb. 8, 1988, now abandoned.

FIELD OF THE INVENTION

The present invention relates to soil purification and in particular tothe purification of soil materials contaminated with organics. Aspecific application of the present invention is for the treatment ofsoils contaminated with organic oils that contain pentachlorophenol(PCP). Such soils are typically found at dump sites from wood treatmentplants.

BACKGROUND OF THE INVENTION

Waste materials from many industries comprise organic materials, oftenorganic greases and oils. In some instances these waste oils includehighly toxic chemicals (contaminants) therein. A well-known example isthe waste material from conventional wood treatment facilities.

At a typical wood treatment facility, wood is preserved by being soakedor dipped in a vat of oil that has a preservative therein. For example,a facility for the treatment of telephone poles, railroad ties, or thelike, may use large vats that contain an oil having pentachlorophenol(PCP) dissolved therein. A typical treatment vat used for such processescontains an organic solution containing about five percent PCP.

Waste organics, often containing a substantial amount of PCP, have oftenbeen dumped into a pit area located near the treatment facility. Whilethis is particularly disturbing with respect to current pollutioncontrol standards, it must be understood that such treatment facilitieshave operated for many decades with substantially little change in theoverall soaking and/or treatment procedure. Thus, many sites exist whichcame into existence well before the more recently imposed pollutioncontrols.

The pollution problem is exacerbated by the nature of the industry. Veryoften a treatment facility was established, short term, near a locationwhere a substantial amount of wood was milled, or treated wood wasneeded. After sufficient operation to accommodate the "local" need, thefacility was closed and sometimes moved to a different location. Thus aplurality of abandoned dump sites exist throughout the country.

Over time, the contaminated organic materials may be transported, bygroundwater, out of the immediate dump area, contaminating a widespreadarea. Since the organics often include a substantial amount of highlytoxic materials therein, this migration poses a substantial health andenvironmental hazard.

It is noted that while the problem of pollution from organics in soilshas been described with respect to a specific industry involving woodtreatment, the problem exists with respect to a variety of industriesthat have similarly generated organic wastes dumped into pits or thelike. The wood treatment industry merely provides a well-known andnotorious example, and one which often involves particularly hazardousPCP.

No satisfactory method of overall soil treatment and/or purification hasbeen previously available. Generally treatment methods have involvedeither incineration alone, microbial treatment, or some combinationthereof. These have not been completely satisfactory, in part for thereasons discussed below.

A frequently used conventional method of purification is incineration.For a typical incineration process, a large incinerator is assemblednear a contaminated site. Soil material is excavated from the site, inbulk, and is incinerated. The incineration process generally destroysmuch of the organic material, but it also results in a large volume ofash material, much of which is fused into hard cakes or blocks. Thismaterial, which may still be substantially contaminated, is typicallythen stored in a secure dump, leaving the excavated site open. After aparticular site has been cleaned, the incinerator is typicallydisassembled and moved to a new location.

Incineration, on its own, has been a generally undesirable process.First it is energy inefficient, that is a large amount of energy isconsumed in operating the incinerator at sufficient temperatures and fora sufficient length of time to lead to effective purification of thelarge volume of materials involved. Secondly, product gases andmaterials from the incineration may be a problem. Further, the largeamount of contaminated ash formed creates a disposal problem.

A second method of purifying contaminated soil is through the use ofmicrobial action. Generally, especially for the oil/PCP problem,microbial purifications have proved undesirable. While in the laboratorymicrobial action may be shown to capably detoxify material, in the fieldit is less efficacious. First, temperature, moisture and oxygen controlmay be essential, and difficult to achieve. Also, a wide variety ofchemical concentrations may be found throughout a single dump site, andfrom site to site. Concentration variations generate unpredictability.Further, complete microbial detoxification of concentrated contaminantsmay take a fairly long period of time, and during that period of timefurther leaching from the dump site may occur. Finally, soil variationsand dump site environment variations pose substantial hurdles to theeffective, predictable, action of microbes.

What has been needed has been an effective method of purifying soil thathas been contaminated with organic material or the like. Generally, tobe effective the method must not only accomplish the desired result,i.e. substantially clean soil, but it also should be relatively costeffective. That is, what has been needed has been a cost effectivemethod to replace, provide an alternative to, or at least operateeffectively in conjunction with, conventional soil treatment processes.

OBJECTS OF THE INVENTION

Therefore, the objects of the present invention are: to provide a methodfor the purifying treatment of soils that have been contaminated withorganic materials; to provide such a method especially suited forapplication to the treatment of soils at dump sites from wood treatmentfacilities; to provide such a method suitable for the purification ofsoil materials contaminated with oils containing PCP therein; to providea preferred such method which involves the utilization and preferablythe superposition of attrition and classification processes to yieldsubstantial removal of contaminating organic materials from solid soilparticles; to provide a preferred such method which further involves astep of flotation separation to further remove contaminated organicmaterial from association with soil material; to provide such a methodwhich yields a concentrated waste material for disposal via conventionalprocesses; and, to provide such a process: which is particularlyflexible for use in association with a variety of sites; which isrelatively simple to effect; which is comparatively cost effective; and,which is particularly well adapted for the proposed applicationsthereof.

Other objects and advantages of this invention will become apparent fromthe following descriptions, taken in connection with the accompanyingdrawings, wherein are set forth by way of illustration and examplecertain embodiments of this invention.

SUMMARY OF THE INVENTION

The present invention concerns the utilization of attrition andclassification processes to yield cleansing of contaminated soil, toremove contaminating organics such as PCP-contaminating oils therefrom.An attrition process is a scrubbing step. Generally in an attritionprocess a slurry containing a high percent of solids is subjected tohigh intensity agitation. During such a process a high number ofparticle/particle contacts occur. This tends to break up the particles,which may be weakly agglomerated due in part to the contaminatingorganics. The particle/particle interactions also help scrub or polishparticle surfaces free of the organics.

A classification process is a process of particle size separation.Typical classification processes include: size separations based onrelative settling velocities in a fluid, such as water; filtration; and,screening. Preferred classification processes for use in applications ofthe present invention are those in which separation is based on relativesettling velocities. These include: centrifugation; flocculation;cycloning; and, use of spiral or screw classifiers. Separations withspiral or screw classifiers, and also those with cyclones, areparticularly advantageous, at least because: they are effective,relatively inexpensive and easy to effect; and, they can be operated onrelatively large scales, even with conventional equipment.

When, according to the present invention, a classification process ispracticed on a soil-containing slurry which has been subjected to anattrition process, substantial soil purification is achieved. Ingeneral, what is preferred is that the classification process issuperposed on the attrition process. That is, the classification processis preferably initiated before particles have had a chance to completelysettle from the attrition step. In this manner, separation is moreefficiently conducted. In particular, it has been found that when thisis practiced in a system wherein the classification is of the typeinvolving relative settling velocities, removal of a fraction containingslower settling materials during the classification procedure leads tosubstantial removal of contaminating organics. That is, during attritiona slow settling (typically fine, low density, high surface area)fraction containing relatively fine particles (and which also contains asubstantial fraction of the contaminating organics) is generated; and,classification conveniently removes and isolates this more highlycontamined fraction. This leaves the faster settling particlesconsiderably purified of, or separated from, contaminating organics.

It is noted that in some instances, attrition and separation can becompletely separated in time. However, generally superposition ispreferred.

Even further purification of the soils (i.e. the fast settling fractionfrom classification) may, according to the present invention, beaccomplished using flotation. Flotation is, in general, a processinvolving separation of materials based on relative hydrophobictendencies. Flotation techniques are generally known, for otherpurposes, in various industries, including the mining industry and thepulp industry. They have also been utilized to accomplish liquidseparations. It is a feature of certain embodiments of the presentinvention that flotation techniques have been found to be adaptable tothe removal of organic contaminants from association with soil, in anefficient and economic purification process. As a result, finalcontaminant concentration in a large fraction of the soil can be reducedto a relatively low level, and the contaminating organics can becollected and concentrated for disposal.

A typical overall soil treatment process according to the presentinvention can be visualized as broken into several stages. In a firststage, the soil is excavated from a contaminated site and it isappropriately screened or otherwise treated for the removal of bulkcontaminating items, such as large pieces of wood, metal objects or thelike. Also during this stage the soil material may be sized to aparticular, preferred, size for further operation.

The preferred second stage involves the practice of superposed attritionand classification processes as previously described. This leads to anisolation, concentration, and removal for disposal, of a fractioncontaining small, fine, relatively contaminated soil particles and asubstantial amount of organics. For example, small wood chips which mayinclude a substantial fraction of the contaminating organics, can beremoved at this stage. Also certain relatively fine soil components, forexample, fine clay and silicate materials, may include a substantialpercentage of contaminating organics thereon. These can also be isolatedand separated at this stage. An advantage to the overall process of thepresent invention is that wood materials, fine soil particles, or thelike, which may be relatively substantially contaminated with organicsubstances, or which may be difficult to isolate from an organicfraction, are readily concentrated and isolated during Stage Two, andmay be treated by follow-up incineration, if desired, in an efficientmanner. That is, they can be transported rather easily, and they arerelatively small in volume by comparison to the total bulk of soil atthe site. The result is a relatively small volume of final incineratorash product, which can be more readily handled.

In some applications, a first stage of attrition may be followed by afirst stage classification, which is followed by a second stageattrition, etc. until a desired level of soil cleansing is obtained.

In a third stage, for some applications, the soil material is treatedvia flotation, for the removal of substantial amounts of remainingcontaminating organic materials from association with the soil. Theflotation process generally involves agitation of the soil as a slurryor suspension, with bubbles of air passing therethrough. Hydrophobiccontaminants, i.e. the typical organic oil/PCP contaminants for example,generally migrate preferentially to the interface with the air bubbles,from the soil surface and/or aqueous suspension. Thus, via flotation theorganic materials may be bumped, rubbed or drawn off the soil and intothe interface with the bubbles. Also, fine particles having asubstantial amount of organics adsorbed or absorbed thereon, and fromwhich scrubbing of organics may be difficult, will also tend to migrateto the interface with the bubbles. Further, liquid organics will tend tomigrate toward the bubbles. These materials are then floated to the topof the flotation system, wherefrom they can be overflowed or skimmed.The contaminants may be readily concentrated and disposed of in aconventional manner, for example by incineration.

It will be understood that a flotation step is not required in allapplications. In some, attrition/classification will be sufficient, toachieve a desired level of purification.

In final steps, the cleansed or washed soil may be returned to the pitarea, or elsewhere, as desired. At this point overall contamination isrelatively low, however further treatment can be undertaken if desired.For example, further washings, flotations, etc. can be used. Also,microbial action may be readily utilized at this point, if desired.

In some applications, flotation may be conducted beforeattrition/classification. Also, it may be intermixed with such steps;for example, flotation after one cycle of attrition/separation butbefore another cycle of attrition/classification.

The present invention, as will be understood from the detaileddescriptions, typically involves use of large amounts of water. Water,for example, is used as a carrier throughout the process, is used toform slurries during attrition and classification, and is also found inthe skimmed material from the flotation process. This water becomessubstantially contaminated with the contaminating organic materialsremoved from the soil. It is an advantage of the present invention thata substantial amount of recirculation of contaminated or potentiallycontaminated water may be provided. It is also envisioned that effectiveoperation of processes according to the present invention will typicallyinvolve cooperation with water treatment processes for substantialpurification of the water used, allowing for recycling of water and/ordischarge to secondary water treatment systems.

The drawings constitute a part of this specification and includeexemplary embodiments of the present invention, while illustratingvarious objects and features thereof.

BRIEF DESCRIPTIONS OF THE DRAWINGS

FIG. 1 is a schematic representation of an overall system for thetreatment of soil according to the present invention.

FIG. 2 is a schematic representation of a flotation device for treatingsoil according to a step of the present invention.

FIG. 3 is a schematic representation of certain alternative ordering ofspecific processes, in a system for the treatment of soil according tothe present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

As required, detailed embodiments of the present invention are disclosedherein; however, it is to be understood that the disclosed embodimentsare merely exemplary of the invention, which may be embodied in variousforms. Therefore, specific details disclosed herein are not to beinterpreted as limiting, but rather as a basis for the claims and as arepresentative basis for teaching one skilled in the art to variouslyemploy the present invention in virtually any appropriately detailedsystem.

ANALYSIS AND CHARACTERIZATION OF SOIL TO BE TREATED

In general, the efficacy of processes according to the present inventionwill depend, in part, upon such factors as: the nature of the organicsin the soil; the nature of the soil particles; the level of toxiccontaminants; and, the final level of purity desired or required.Determinations of whether, and how, to provide processes according tothe present invention in an overall cleanup scheme will depend, in part,upon analysis of the above factors.

A useful analysis in examining the above factors, is to determine thenature of the organics in the soil to be treated. Soil organic matter isdefined as the total of the organic compounds and soil exclusive ofundecayed plant and animal tissues and the soil biomass. It consists oftwo broad categories of substances commonly referred to as humicsubstances and non-humic substances, and includes particulate material.Humic substances are high molecular weight, dark colored, substancesformed by secondary synthesis reactions of soil and sediment. Non-humicsubstances are compounds belonging to known classes of biochemicals,e.g., proteins, carbohydrates, fats and organic acids. Many toxiccontaminants, such as PCP, are observed to partition well into humicsubstances. Thus, if the analysis shows a substantial level of humicsubstances, it can be predicted that substantial amounts of thecontaminants will tend to "follow" the humic materials, throughprocessing.

In general, if there are effectively no naturally occurring organics andno fine particulates such as clays in the soil, the soil washingtechniques according to the present invention will be relativelyeffective over all particle sizes in the soil material. Materialscontaining relatively little or no naturally occurring organics and nofine clays might include, for example, river gravel or beach sand. Whensuch materials do include relatively little or no naturally occurringorganics, silts or clays, contaminants are relatively readily scrubbedor washed from the particle surfaces, and the scrubbing (attrition)techniques described below are very effective in yielding purification.

However, in many applications the soils do contain natural organics andfine soil particles. A typical natural level for naturally occurringorganics, in soils, is about 1 to 2 percent. If the naturally occurringorganics and other fine soil material are present at about this level orhigher, an examination of the soil particle size is desirable, toevaluate efficacy of soil washing processes according to the presentinvention. A reason for this is that naturally occurring organics appearto facilitate association of the contaminants with soil particles,particularly those soil particles of relatively small size.

A first, gross, analysis is to evaluate the fraction of the soil to bepurified, that comprises greater than about 10 to 20 mesh components(i.e. components that will not pass through a screen filter of about10-20 mesh). The mesh components greater than about 10-20 mesh can bereadily separated by techniques such as screening and the like. Such aninitial, rough, screening not only separates out rocks and pebbles, butalso pieces of wood and the like. In many instances separation of woodchips or the like will result in considerable reduction in thecontaminating organics, since the contaminating organics oftenselectively partition into such materials. In the unlikely event thatthe great majority of the contaminating organics are associated withmaterial of greater than about 10 to 20 mesh, all that might benecessary to achieve significant soil purification would be removal ofthe 10 to 20 mesh fraction, which can be accomplished by screeningmethods. On the other hand, if analysis shows that there is significantcontamination of the less than about 10 to 20 mesh fraction, furtheranalysis is necessary; and, the attrition/classification processdescribed herein below may be of utility.

A next desirable evaluation, is to determine the relative amount ofabout 10 (or about 20) to 200 mesh material (versus smaller than about200 mesh); and, to determine the approximate (and relative) level ofcontamination in the 10 to 200 (or 20-200 if 20 mesh is used as theupper limit) mesh material. A primary reason for this is that smallerthan about 200 mesh (i.e. 74 micron) material particles are not readilypurified utilizing the soil scrubbing (attrition) techniques describedherein. While there may be a number of reasons for this, and applicantsdo not wish to be held to any particular theory, it appears that ifparticles are smaller than about 200 mesh (i.e., smaller than about 74microns), then during a high shear attrition processes, the particles,in solution, do not attain sufficient momentum for their collisions toresult in significant scrubbing or abrasion of the particle surfaces.That is, the scrubbing processes, as utilized in the present invention,(typically attrition scrubbing), rely upon particle collisions tofacilitate abrasion of the particle surface and cleansing. If theparticles are too small, typically less than about 200 mesh, they do notappear to sufficiently collide in the attrition scrubber to rendersignificant cleansing. Thus, if there is relatively little contaminationin the about 10-20 mesh to 200 mesh fraction, (compared to the smallerthan 200 mesh) rather than scrubbing, what is generally desired (forpurification) is merely a classification to obtain a removal of thefraction at about 200 mesh or smaller, for disposal via techniques suchas incineration and/or biomanagement. If, as is more likely the case,there is significant contamination in the about 10-20 mesh to 200 meshfraction, then the soil will generally be susceptible to significantcleansing via attrition/classification operations, such as those of theinvention described below.

Several other factors are, however, significant. If, for example, theless than about 10-20 mesh material includes greater than about 50% ofmaterial sized smaller than about -200 mesh, the less than 10-20 meshmaterial is not as readily susceptible to soil washing techniques as itwould be if it contained less than 50% particles smaller than about 200mesh material (and preferably less than about 30-35% of such material).A reason for this is that during the washing and handling steps,materials that contain such a high percentage of fines will tend to forma thick, sludgy, filter cake which is relatively difficult to handle.

For more refined soil cleaning processes, it is desirable to determinethe amount and nature of the 10 micron to 74 micron fraction in thesoil. While such material is not as readily susceptible to washing byattrition scrubbing and the like, (since collision among the particlesin the solution may be a problem), if the fraction is relatively clean,or only a small percentage of material within the fraction is present inthe less than about 10-20 mesh particles, it may be carried through andkept with the cleansed material. That is, following the attritionscrubbing, as indicated above and as described in the further detaileddescription below, there is a classification step. In general, theclassification step will be set to retain particles above somewherebetween about 10 and 74 microns within the "cleansed" material. If thefraction between about 10 and 74 microns is significant, and contains asignificant percentage of contaminants, then the classification stepsshould be set to only cut materials at about 74 microns or above intothe "cleansed" fraction. On the other hand, if the fraction betweenabout 10 and 74 microns comprises only a relatively small percentage ofthe material less than about 10 to 20 mesh, then even if it isrelatively contaminated it might be tolerated in the overall "cleansed"material (since it would not contribute significantly to overallcontamination). Also, even if a significant percentage of materialbetween about 10 and 74 microns is present in the overall less thanabout 10 to 20 mesh fraction of particles, as long as it is less thanabout 50% (for the handling reasons as discussed above) and isrelatively uncontaminated, it can be carried through with the "cleansed"material. Thus, it will be understood, in either of the latter twodescribed instances a classification technique can preferably beutilized which takes, with the "cleansed" soil, material at about 10microns or greater.

In general, it will be desireable to set the classification so that assmall a particle size as can be tolerated is maintained in the"cleansed" material. A reason for this is that it reduces the amount ofsolids which must be handled in the waste stream. Thus, if the "cut" canbe taken at about 10 microns or larger (as opposed to about 74 micronsor larger) without unacceptable levels of contamination in the cleansedproduct, it will be preferred.

In general, taking a "cut" at about 74 microns or larger can beaccomplished utilizing a countercurrent screw classifier system, asdescribed in detail below. Taking a "cut" at a selected size betweenabout 10 microns and 74 microns is accomplished through application oftechniques such as hydrocycloning.

The very finest fraction (less than about 10 microns) does not readilysettle from suspension. It will typically be carried with the wastestream from the classification step. This is preferred, as generally itis quite difficult to separate such materials from organic contaminants.

STAGE 1 Initial, Rough, Screening and Separation

As previously indicated, the present invention is described herein forapplications involving the treatment of soil and materials found at dumpsites from wood treatment facilities. It will be understood, however,that the principles of the present invention are generally applicable tosoils and similar materials contaminated with a variety of organics froma variety of processes. Thus, the specific treatment described herein isto be considered exemplary only.

In the first stage of the operation, excavated material from the dumpsite is physically treated so that it can be readily handled during thelater purification washes and other steps. That is, any largeunmanageable materials such a large rocks, tree stumps, scrap metal orthe like are removed. Typically, to accomplish this, the soil materialis physically removed from the dump site, and is passed through ascreening device, such as a grizzly. In this apparatus the bulkcontaminating materials such as pole butts, large wood blocks, or thelike are removed from the soil. One reason why such a pretreatment ofthe soil is often desirable is that in many instances organic dump sitesare also used as dump sites for waste items such as old tires, unusablepieces of wood, machinery parts or the like.

Typically, soil material which passes through the grizzly includes alarge amount of chunk or agglomerated material, i.e., material stucktogether in large clumps or clods. While concentrations may varyconsiderably, from a typical wood treatment waste dump this soilmaterial typically includes a pentachlorophenol (PCP) concentration ofabout 100 to 2000 parts per million. This substantial concentrationoften results from a concentration of oil and grease in the soil ofabout 0.1 to 1.0 percent by weight. The oil and grease may actually beadsorbed upon certain components of the soil, or it may simply betrapped in the clumps, or it may simply be associated with certainfractions in the soil from which separation is difficult. The PCP, onthe other hand, is typically found merely absorbed, or dissolved, in theoil materials. That is, it is often not directly adsorbed onto the soilitself. Thus, removal of the oils or greases along with those componentsof the soil either having a disproportionate amount of oil or greasetherein or from which separation of the oils or greases is difficult,leads to substantial removal of the highly toxic contaminant (PCP).

The soil material at this point of the process typically containsseveral components. First, it often contains substantial amounts ofsmall wood pieces. It is found that these wood pieces usually include arelatively and disproportionately high concentration, of contaminatingorganics (for example 1500 to 2000 parts per million PCP) therein. Theprecise physical nature of this contamination is not known; however, itwill be readily understood that it is desirable to selectively removethis wood component. A substantial portion of the wood component isremovable during a first stage pretreatment process in several manners.

First, the soil material from the grizzly is conveyed into aconventional trommel or mill to substantially break up the clumps ofdirt materials. In the trommel, the material is sprayed with water, tofacilitate the breaking-up process and the removal of undesiredcomponents.

The slurry or sludge from the trommel is then preferably passed ordischarged onto a screen system, to further size the materialdownwardly. Generally, a screening at about 10-65 mesh (preferably about10-20 mesh) is desirable. Multiple screening steps may be used. Furtherwater may be added to facilitate the screening process.

In a typical operation, the total amount of water added during both thetrommel and screening processes is such as to result in about 10-60%solids, by weight, and preferably less than 50% solids. The splitbetween water addition in the trommel and during screening may be asnecessary to facilitate the two processes. It will be understood that avariety of amounts of water may be used, the above merely generallyrepresenting operable figures.

A substantial amount of wood material, which is not substantiallybroken-up during processing in the trommel and washing through about10-65 mesh (or smaller) screens is removed at the screening stage. Thisconcentrated wood material can be collected and readily incinerated, orotherwise treated for disposal. It is a particular advantage to thepresent invention that small pieces of contaminating wood, with organiccontaminants absorbed therein, are readily concentrated, for disposaltreatment via processes such as incineration. That is, the presentinvention concerns isolation, into a relatively small volume, of thosematerials or fractions which contain a high amount or concentration ofcontaminating organics. These may be relatively efficiently incinerated.

FIG. 1 is a schematic representation of a process according to thepresent invention. Although the following descriptions focus on themovement of soil materials, it is noted that the scheme depictedincludes an advantageous system of water flow, making efficient use ofcontaminated water. Referring to FIG. 1, the reference numeral 10generally designates stage 1 of the process. Reference numeral 11illustrates a step of loading contaminated soil into grizzly 12, forinitial separation. Large contaminants, such as pole butts and the like,are removed at 13. The material which passes through the grizzly 12, isconveyed into a trommel 14 and is broken therein. Reference numeral 15generally designates flow of water into the trommel, to provide forproduction of a slurry. The slurry flow out of the trommel is designatedby reference numeral 16. This material is directed toward a screeningsystem 18, preferably comprising at least a 10 mesh screen 19 and insome applications preferably also comprising a 20 mesh screen 20. Theslurry material is directed through the screen system 18, with aid ofwater provided as indicated at reference numeral 25. It is noted thatfluid feeds 15 and 25 may be provided from a single source 26, withconventional valves or the like controlling relative distribution offluid into the trommel 14 and the filter system 18. Large materials suchas wood chips or the like removed from the filter system 18 are showntakenoff at reference numeral 30. The soil material which passes throughthe screen system 18, sized to 20 mesh or smaller, is generallyindicated at takeoff 31.

STAGE 2 The Attrition and Classification Procedures

The material removed from a physical screen such as system 18 may stillbe substantially clumped or agglomerated. At this point a typical soilmaterial generally comprises numerous components including: stillsmaller pieces of wood material; clay components; silica sand and otherrelatively coarse minerals; and, natural organic matter such asdecomposing plant material or the like. Due in part to the presence ofthe oils and greases in the contaminants, this soil material may stillbe clumped into relatively hard globules, preventing release ofcontaminants from between trapped inner particles. In a preferredapplication of the present invention the slurry of this material isconcentrated (thickened) substantially, in a cyclone or the like, toabout 40-70% solids, or more, and is then broken up and scrubbed in anattrition step, such as in a pebble mill, attrition cell, or the like.During attrition, the slurry of solids is subjected to intenseagitation. This suspends the solid particles, and causes a great deal ofparticle/particle collisions. The collisions break up the agglomerates,resulting in suspended particles of a variety of sizes. Some of thecontaminating organics are abraded off of the particles, and aredispersed in the water.

It has been found that a fine particle soil component, which for somesoils is a relatively small percentage component by weight or volume, issometimes associated with a substantial and disproportionate percentageof the contaminating oil and grease, with the contaminant (for examplePCP) therein, by comparison to the coarser components (sometimes themajor component) of the soil. While it is not intended that thisinvention be limited to any particular theory, it may be theorized thatthis phenomenon may be due in part to the fact that fine particlespresent relatively large surface areas on which organics can readilyadsorb. It may also be that the relative difficulty of separating offine particles from non-adsorbed organics is in part responsible for theobservation. In any event, generally a separation out of very fineparticles, with any organics (absorbed or otherwise) associatedtherewith, results in substantial purification of the remainingmaterials (i.e. the "cleansed" or "washed" materials).

As described above, in general attrition scrubbing is effective onparticles of about 74 microns (200 mesh) or larger, up to about 10 mesh.When the particles are significantly smaller, especially if less thanabout 10 microns, they do not appear to be readily cleansed duringattrition scrubbing. This may be, in part, due to an inability of suchparticles, in aqueous suspension, to attain sufficient momentum forparticle/particle collisions to effect a good, scrubbing, action. Withparticles of about 74 microns (200 mesh) up to about 10 mesh, on theother hand, attrition scrubbing results in an effective scraping of thesurface of the particles, and thus a removal of organic contaminantstherefrom.

While a variety of methods for cleansing the surface particles areknown, including the use of vibrational energy, application of highpressure water jets, and use of washes with detergents (surfactants) andthe like, the attrition scrubbing techniques described herein appear toyield a significant advantage. A reason for this is that attritionscrubbing generates relatively complete access to the surface of theparticles. That is, in time much of the outer surface of the particleshas been actually abraded somewhat, removing any contaminating layer andreleasing it to suspension. The contaminating layer, it will beunderstood, is readily removed in the follow-up countercurrentclassification step.

It is a feature of certain preferred embodiments of the presentinvention that the follow-up classification step is practiced afterattrition, but before substantial settling, i.e., it is superposed onthe attrition step. This is not required for the achievement of someadvantages, but it does generate a more efficient separation. Duringclassification, advantage is taken of the fact that large, low(relative) surface area particles settle faster than very fire(relatively high surface area) particles. In general, the very fineparticles (for example, clay) liberated during attrition and whicheither have much of the organics adsorbed thereon, or in associationtherewith, are separated by classification, resulting in separation andremoval of a substantial percentage of contaminating organics. Again, aswas described above, the very finest materials (i.e. smaller than about10-74 microns) were probably not readily scrubbed clean in the attritionstep. It is also noted that natural organics in the soil may alsoinclude fine particulates and be disproportionately contaminated. Thesewill also be removed by the classification techniques described, leadingto some further purification.

The material from the attrition scrubber or pebble mill is directed, forexample, into a classification system. Preferably a classificationsystem relying on relative settling velocities is used, such as a screwclassifier, or a plurality of screw classifiers in series, with awashing water flow directed countercurrent to movement of the soil.Alternate methods include the use of cyclones. The washing waterremoves: relatively small, slow settling particles of wood; small, slowsettling particles of soil such as clay having substantial amounts ofcontaminant associated with it; and/or, floating or suspended organics.The contaminants removed by washing can be collected, concentrated andtreated, for example via incineration or the like. It is an advantage ofthe present invention, again, that those components of the soil whichare not as readily purified of, or isolated from, contaminatingorganics, but which generally comprise a substantially small volume ofthe soil, are separated and concentrated, so that they may be treatedvia conventional disposal techniques, such as incineration, in anefficient and effective manner.

It will be recognized that conventional screw classifiers may beutilized during this step. They are especially useful if the "cut" is tobe taken at about 200 mesh (74 microns) and above. That is, they areparticularly useful if particles smaller than about 74 microns are to bekept with the waste slurry, and larger particles are to go with thecleansed solids. This will be the case if the particles of less thanabout 74 microns are perceived to present a significant contaminationproblem due to the fact that they (due to their small size) are notreadily cleansed during soil washing (attrition). A variety of washingwater flow rates may be utilized, depending on the system to which theprocess is applied. Generally, a percentage range of solids in the screwclassifier(s) of about 10-50% is effective. For a typical purificationof soil from a PCP dump site, material entering the first screwclassifier could include about 100-200 parts per millionpentachlorophenol. In most applications, the purification process isapplied for a period of time sufficient for reduction of organiccontaminant to reach a readily achievable minimum. An advantage of thepresent invention is that, for specific operations, stages can be variedin order to achieve an overall most efficient, or at least substantiallyefficient, operation.

The soil material (dewatered) from a typical screw classifier step,according to the present invention, includes about 75% soil, by weight,the remainder being substantially water. At this point, the soilgenerally comprises primarily silica sand or other coarse materials withsome oil or grease thereon, much of the wood component having alreadybeen removed as well as a substantial portion of the fine clay or silicacomponent and any floatable natural organic components. In someinstances, some of these materials will still be present, however, andfurther cleansing with respect to them may be accomplished in a thirdstage treatment.

As explained above, in some applications it may be desirable to take a"cut" at closer to about 10 microns, or at some point between 10 and 74microns. That is, in some applications particles of a size greater thanabout 10 microns (or some other figure between 10 and 74 microns) are tobe maintained with a "cleansed" fraction. In general, screwclassification systems are undesirable unless the cut is to be taken atabout 74 microns. When a cut of the smaller particle size is desired,hydrocycloning techniques may be employed. In general, as indicatedabove, a cut at a point below about 74 microns, and down to about 10microns, may be desirable if there is a substantial fraction of soilmaterial within that particle size that is not contaminated to such anextent that the overall resulting "cleansed" soil will have aconcentration of contaminant above the acceptable level. That is, whilethe 10-74 micron fraction will not be readily cleansed during theattrition scrubbing operation, it may be carried through with thecleansed material if it does not pose a substantial contamination threatto the final material. Operation in this manner will tend to reduce theamount of solids in the waste water stream that have to be dealt withduring waste water treatment.

Referring to FIG. 1, underflow from the screen system 18 is showndirected into cyclone 32. Overflow liquid is removed via line 33, andthe soil slurry is transported via line 34 to attrition equipment suchas an attrition machine 35. After sufficient, or desired, breaking up ofthe sludge material, and before substantial settling occurs, the finerproduct is transported to classification system 40 via line 41.

For the preferred embodiment described and shown, the classificationsystem 40 comprises a plurality of classifiers arranged in series, witha countercurrent wash flow. More specifically, conventional screwclassifiers 42, 43, 44 and 45 are shown arranged in series. As thedewatered soil is transported along the classifier circuit via lines 46,47 and 48, a countercurrent flushing or washing water flow, to generallyremove wood, natural organics, and slow settling, fine materials such asclay, occurs via flow lines 50, 51, 52 and 53, respectively. Thecontaminated wash material is removed from the system via line 55. Thewashed, coarser, fraction, typically primarily a silica sand or othercoarse mineral component, is removed from the system via line 56,whereby it is transported into Stage 3. Attrition devices may beinserted between steps of classification, to facilitate the soilpurification process, for example water flow from line 52 could becombined with dewatered soil from line 46, for delivery to an attritiondevice such as machine 35. The effluent from the second attrition wouldthen be directed into classifier 43.

Referring to the schematic of FIG. 1, it will be understood that thewash flow from the classifiers, through line 55, may be directed throughscreen 56', to lead to concentration of solid materials which can beremoved via line 57 for incineration. Contaminated water released fromthe filter system 56', via line 58, may be directed into Stage 3 foruse.

A variety of conventional classifying equipment may be adapted forutilization in processes, according to the present invention. Ingeneral, adjustment of appropriate operation parameters for themachinery or equipment, to achieve a desired "cut" or separation, is amatter of following manufacture specifications, or direction from themanufacturer's applications engineers. The following is a brief list ofsuppliers of equipment adaptable for use in applications according tothe present invention. The list is not intended to be exhaustive.

Spiral classifiers: Denver Equipment Company, Colorado Springs, Colo.;McLanahan Corporation, Holidaysburg, Pa. Hydrocyclones: Krebs Engineers,Menlo Park, Calif.; and, Dorr-Oliver Incorporated, Stamford, Conn.

In general, the operatings parameters for the above-classificationdevices will be with a feed slurry containing solids in a range of about10-50% by weight. Other process variables, for example the spiralclassifier rake rpm or hydrocyclone apex diameter, will depend on thespecific machinery utilized. Tests during start-up of the equipment canbe performed to further optimize these parameters, for a particularapplication.

In some applications, vibrating screens may be utilized to assistseparations based on particle size. Manufacturers and/or suppliers ofVibrating Screens include: Derrick Manufacturing Corporation, Buffalo,N.Y.; and, Diester Machine Company, Fort Wayne, Ind.

STAGE 3 Separation of Organic Material from Soil Components by Flotation

Flotation processes are known in the mineral industry and the pulptreatment industry; see for example, Froth Flotation--50th AnniversaryVolume, Ed. by Fuerstenau, D. W., American Institute of Mining,Metallurgical, and Petroleum Engineers, Inc., New York, 1962; Flotation,Volumes I and II, Ed. by Fuerstenau, M. C., American Institute ofMining, Metallurgical, and Petroleum Engineers, Inc., New York, 1976;Chemical Engineer's Handbook, 5th Ed.; Ed. by Perry, Robert F.,McGraw-Hill Book Col; New York 1973, pp. 21-65 to 21-69; Wills, B. A.;Mineral Processing Technology, Pergamon Press, Oxford, 1979, pp.276-337; and, Zimmerman, R. E. and Son, S. C., "Part 3: FrothFlotation", Coal Preparation, 45th Ed., E. by Leonard, J. W., AmericanInstitute of Mining, Metallurgical and Petroleum Engineers, Inc., NewYork, 1979; the disclosures of which are incorporated herein byreference. Flotation may be provided in a variety of machines.Generally, flotation process machines are separated into two basiccategories, mechanical flotation machines and pneumatic flotationmachines. Within each category are two types, those operated as a singletank, and those operated as a bank of tanks (or cells) in series.Virtually any flotation system may be optionally utilized in associationwith the present process; however, generally preferred processes willinvolve the use of a mechanical flotation device, either alone or inseries with other such devices. It is noted that final flotation steps(polishing steps) may not be required in some purification schemes.

The primary function of a flotation separation in an application to thepresent invention is to allow hydrophobic contaminants to contact andadhere to air bubbles. The air bubbles rise to the top of the flotationdevice, carrying the hydrophobic material with them. This generallyresults in formation of a contaminated froth at the top of the solution,which can be overflowed, skimmed or otherwise removed. As a result, thesolid material contained within the flotation tank or cell issubstantially purged of the hydrophobic material.

A unique application of a flotation technology is involved in preferredapplications of the present invention. In particular, the processinvolves the removal of organic contaminants from soil, and separationof soil particles not readily dissociated from organics, from theremainder of the soil. The organic components, including the greases,oils and any dissolved PCP or other toxic organics, are typically veryhydrophobic and thus susceptible to removal via the flotation process.Generally, what is required is that the machine maintain the soilparticles in suspension and further that the system generate sufficientdispersion of air bubbles throughout the solution, with collision of airbubbles with particles, to ensure high frequency of contact between theair bubbles and the particles for substantial transport of hydrophobicorganic material to the air bubble surface.

Generally, a concentration of about 10-40% solids, by weight, in theflotation step is effective. Preferably high solids concentration,and/or intense agitation, are avoided so that little attrition(particle/particle collision) occurs. A reason for this is thatattrition would tend to pull bubbles off of floated particles, thusallowing less time for transport of organics to the bubbles.

A variety of manufactures of flotation equipment can be utilized inassociation with processes according to the present invention. Theseinclude, for example, flotation machines developed for other uses,operated with appropriate stirring velocity and air bubble flow. Suchdevices include systems which generate air bubbles by a simple draw ofair from the atmosphere, and also those which utilize separate blowersor pressurized air sources. Usable flotation machines or cells areavailable, for example, from the Denver Equipment Division, JoyManufacturing Company, Colorado Springs, Colo. 80901; Outokumpu Oy,Espoo 20, Finland; and, Wemco, Sacramento, Calif. 95852. Such devicesare generally developed for use in the mining industry; however, theycan be readily adapted to application according to the presentinvention.

Referring to FIG. 1, Stage 3, i.e., the flotation stage is generallyindicated at reference numeral 60.

Once pretreatment at Stage 2 has rendered a sufficiently purified soilmaterial, the soil material is transferred into a flotation cell 61, asfor example along flow path 62. As indicated previously, when, forexample, a series of screw classifiers is used to wash and transfersufficiently ground up or otherwise sized particles of soil, from atypical pole treatment dump the washed material comprises about 85-95%soil by weight, and contains 5-20 ppm PCP. The material is directed intoa flotation cell 61, along with a sufficient amount of water via line 63for cell operation. Agitation is started, and is maintained at a rateappropriate to inhibit any substantial settling of material, i.e., thatis a sufficiently high rate to maintain substantially all particles insuspension. Air bubbles are formed in the flotation cell, duringoperation. These air bubbles, typically numerous micro bubbles, may beformed by an atmospheric draw, or through the provision of a blower orsource of pressurized air or the like. Generally sufficient bubbleformation is created to ensure effective flotation of the organicmaterial from the soil material, for effective purification. The organicmaterial trapped in the air bubble froth is floated to the top of themachine, wherefrom it can be removed by overflow or by use ofconventional mechanical skimmers or the like, along path 64. Similarly,any fine soil particles having organics adsorbed thereon will also tendto flat to the froth.

For Stage 3, reference numeral 60, shown in FIG. 1, a second flotationcell 70 is shown used in series with the first cell 61 to achieve a highdegree of cleansing. The underflow from cell 61 is directed to cell 70along flow path 71. Water, for froth formation, is directed into cell 70via line 73. The overflow or froth is removed at 74, and the underflow,or purified soil, at 75. The clean soil is separated from the water at76, and is removed at 77. The carrier water is removed at 78, and may becycled into backwash for Stage 2.

In the preferred embodiment shown, froth, from 64 and 74, isconcentrated while the water removed therefrom is directed into a waterpurification system 80. The purified water may be stored in reservoir81, and used throughout the process.

In FIG. 2, a typical flotation cell for use in a system according to thepresent invention is schematically depicted. In FIG. 2, the cell isgenerally designated at reference numeral 100. The cell 100 includes atank portion 101 into which water and contaminated soil, typically as aslurry, are dumped for treatment. The sludge or slurry 102 within tank101 is rapidly agitated by an agitator/aerator 103. The particularagitator 103 shown includes a plurality of vanes 105 thereon whichrapidly rotate to churn the water, and keep the solid soil material fromsettling in the bottom of the tank. Air bubbles are formed in a highsheer zone between the agitation cones 105 and the stator, with air flowbeing generally represented by arrows 107. As the bubbles dispersethroughout the slurry or sludge 102, soil particles are encountered,organics transfer to the interface with the air bubble, and the organicsfloat to the top of the tank in the form of froth 110. The froth is thenremoved via skimming or overflow 111, as indicated at reference numeral112. The three components which are mixed in the tank (air, soil andwater) are represented as being introduced via lines 115 and 116,respectively. Underflow is shown removable via the port 120, operated byvalve 121.

It will be understood that FIG. 2 is intended to be schematic only, andthat a variety of specific mechanical structural arrangements can beutilized.

In systems according to the present invention, agitation speed, airbubble size and concentration, water concentration, and retention timein the tank may be varied to achieve an optimum, or at least a desiredlevel of efficiency and purification. It is noted that the flotationcell may be operated on a closed, batch, cycle, or with a continuous runtherethrough. Generally, a continuous system will provide for a moreefficient overall operating system.

Referring again to FIG. 1, underflow from the flotation system isgenerally designated at reference numeral 75. This material includes thepurified soil, generally containing less than 10 ppm PCP, and preferably5 ppm PCP or less. At this relatively low concentration, the PCP maypose substantially little problem. If desired, in some applications ofthe present invention this soil can be dried and transferred back to thepit area with an active microbial agent therein, to obtain even furtherpurification.

The skimmed or overflow material from the flotation cell can beconcentrated, if desired, and incinerated. The water, somewhatcontaminated, can be directed to a water treatment facility or the like.

Frothers may be added during flotation. Frothers generally change thesurface tension of the water in a manner facilitating formation of astable froth phase. Frothers include methyl amyl alcohol and pine oil.They may typically be used in an amount of about 0.01-0.2 lbs.frother/ton of soil in the flotation device.

The Embodiment of FIG. 3

In some applications of the Stage 2 process, it may be desirable toapply the attrition equipment and classifier equipment in series, suchthat a first attrition step is followed by a first classification step,which is followed by a second attrition step, that is followed by asecond classification step etc., until attrition/classification isachieved to a desired extent. A flow diagram representing an example ofthis, is presented in FIG. 3. it will be understood that much of theequipment used in a process according to FIG. 3 may be as describedabove for FIG. 1.

Referring to FIG. 3, reference numeral 331 designates the underflow froman initial screening process, analogous to underflow 331, FIG. 1. Thesoil material in this underflow 331 is fed into cyclone 332, analogouslyto FIG. 1, for thickening. Overflow liquid from cyclone 332 is directedvia line 333 outwardly from the cyclone 332. This material may bedirected analogously to the material in line 33, FIG. 1.

The thickened soil slurry from cyclone 332 is directed via line 334 intothe attrition/classifier system (Stage 2 system) generally representedat 334' System 334' includes an initial attrition device 335 into whichthe soil slurry is fed, via line 334. In an attrition device 335 theslurry is subjected to attrition, as described above with respect todevice 35, FIG. 1. Material from attrition device 335 is selectively fedvia line 341 into cyclone 342. (A valve arrangement can be used tocontrol flow.) The underflow (larger material) from cyclone 342 is fedinto a second attrition device 345; and, the underflow, (largermaterial) from cyclone 343 is fed into attrition device 346. Afterattrition in device 345, the material may be fed via line 347 into thesecond cyclone 343, with the heavier, larger, material ultimately beingfed into second attrition system 346. Feed from the second attritionsystem 346 may be selectively fed via line 350 into cyclone 351. Theunderflow from cyclone 351 is shown being drawn off at line 352.

Selected and controlled flow through the system 334' is generallycontrolled by valves 355, 356 and 357. The finer materials from cyclone343 are shown drawn off through line 360, and those from cyclone 351 areshown drawn off at line 361. Transport from attrition device 335directly to the second cyclone 343 is shown controllable via valve 355,and line 370. (Line 371 may be used to provide a countercurrent wash.)Similarly, flow from attrition device 345 into cyclone 343 and 351 iscontrollable by valve 356, via line 373; and line 374 can be used toprovide a countercurrent wash. Valve 357 controls flow from attritiondevice 346 into cyclone 351, via line 377; and, line 378 allows for feedof countercurrent wash. Overflow, i.e. fines, from cyclone 342 is shownbeing drawn off via line 380. Line 381 may be used to provide a washwater feed to cyclone 351.

It will be readily understood that the configuration of FIG. 3,illustrates that attrition devices and classifiers may be interposedsuch that a first attrition step is followed by a classification step,followed by a further attrition step and further classification stepetc., to achieve beneficial results. It will be understood thatalternate classifier systems, for example screw conveyors, may be usedin place of some or all of the cyclones at 342, 343 and 351. Also, it isnot intended that the flow arrangement need necessarily be asillustrated, or that there necessarily be three attrition devices(rather than more or fewer) in the system. Rather, the arrangement ofFIG. 3 is exemplary of a superposition which involves a plurality ofalternating attrition/classification steps.

pH Control; Surfactants; Temperature Control

The general process has been described in the absence of specificadjustments in pH, and without the use of added surfactants. Generally,for many soil treatment processes according to the invention, effectiveremoval of organic contaminants can be obtained without special pHadjustments or surfactant use. Should it be deemed necessary, a pHadjustment can be made at almost any stage. Also surfactants can beintroduced at various stages to facilitate removal of the organicmaterial from the solid particles. The process is generally effective atambient temperatures, but may be practiced over a wide variety oftemperatures. In some instances temperature control may be used tofacilitate certain steps.

Mobile Testing Facility

The previously described process is very flexible. That is, it can beimplemented using fairly conventional process equipment, when theequipment is organized for operation in the unconventional mannerdescribed. The particular equipment to be used may vary depending on thespecific nature of the soil being treated, and the specific nature ofthe contaminant contained therein. As soil composition and particle sizeranges and contaminant concentration and nature vary, individualspecifics of the treatment may be changed accordingly. For example, insome systems, a single flotation cell may be all that is needed toaccommodate efficient purification, whereas in still other systems aplurality of cells in series may be required.

Generally, it will be preferred to evaluate a particular site to betreated, in advance of setting up a full scale treatment facility, inorder to determine what specific equipment will be necessary. Toaccomplish this, a mobile, pilot scale facility may be provided,utilizing appropriately mounted equipment arranged to conduct a processaccording to the present invention on a small scale. Via such anarrangement, an evaluation of the soil can be made. In this manner, amost efficient utilization of the treatment process, can be determined.

Operation of the present process will be further understood by referenceto the following experiments and examples.

EXPERIMENT 1 Characterization of Soil Contaminated With PCP

For the following experiment, contaminated soil collected from the dumpsite of a pole treatment plant was utilized. The two major impurities ofconcern were pentachlorophenol (PCP) and the grease/oil component. Thesoil sample contained a substantial amount of wood therein. Originallythe soil, classified to less than one-half inch, contained about 18%water. The overall PCP concentration in the sample was about 250 ppm.The sample contained a variety of sizes of particulates and could besized accordingly. It was generally found that the PCP concentrationvaried throughout the size range of the particles, being higher in sizefractions coarser than 20 mesh and finer than 150 mesh, as shown inTable 1. The data suggested that a two-step process of coarse screeningand fine screening or classification may significantly clean the bulk ofthe soil by removing a small fraction of the original material that ishighly concentrated with PCP. Wood concentration in the soil sample wasfound to be about 5-10% by weight, with the bulk of the wood beingcontained in larger chunks or pieces. The grease/oil concentration wasgenerally about 40-80 times greater than that of the PCP concentration.

                  TABLE 1                                                         ______________________________________                                        Typical Distribution of Pentachlorophenol in Soil                                      Sample Weight                                                                             PCP Concentration                                        Screen Size                                                                             Grams     Wt. %    ppm                                              ______________________________________                                         3M        13.4     1.33     301                                               6M        62.6     6.23     424                                              10M        29.6     2.95     715                                              20M       302.8     30.14    310                                              35M       186.2     18.53    222                                              65M       204.4     20.34    124                                              100M      114.7     11.42    120                                              150M       49.2     4.90     141                                              -150M      41.9     4.16     504                                                        1004.8    100.00%                                                   ______________________________________                                    

EXPERIMENT 2 Dry and Wet Screening

This separation step was undertaken to eliminate handling difficultiescreated by the wood content of the soil and to confirm PCP distributionin the soil. The process involved screening to -10 or 20 mesh to removethe bulk of the coarse wood, and is described above as occurring inStage 1.

The test soil was subjected to both dry and wet screening. The dryscreening was merely a cursory test to remove the bulk of the coarsewood. For the dry screening, the soil sample was first dried at 75° C.to at least 16 hours. The dry soil was then screened through a 10 meshscreen, using a manually shaken, frame-mounted screen. The +10 mesh and-10 mesh fractions were analyzed for PCP. The dry screened materialshowed a significant and disproportionate accumulation of PCP in the +10mesh fraction, which was determined to contain a significant amount ofwood. The results of this screening are reported below in Table 2.

                  TABLE 2                                                         ______________________________________                                        Assay of Fractions from Dry Screening                                         Fractions   Weight (g)                                                                              Weight (%)    ppm PCP                                   ______________________________________                                        +10 mesh     3,450    10.4          547.5                                     -10 mesh    29,800    89.6          328.3                                     ______________________________________                                    

For the wet screening, a weight of tap water equal to the weight to bescreened was poured into a large tub. Portions of the soil were placedon a frame-mounted 10 mesh screen which was shaken while partiallysubmerged. The +10 mesh fraction that remained on the screen was thenwashed with as little water as possible, and collected. The process wasrepeated until all of the soil sample was screened. The +10 mesh portionwas dried and sampled for analysis of PCP. A second sample of this dried+10 mesh product was screened into five separate size fractions. Typicalassays of fractions derived from screening the +10 mesh product arelisted in Table 3.

                  TABLE 3                                                         ______________________________________                                        Assay of Fractions Derived from the +10 Mesh Portion                          Obtained by Wet Screening                                                     Fraction Size (Mesh)                                                                            ppm PCP                                                     ______________________________________                                         +3M              856                                                          +6M              503                                                         +10M              472                                                         +20M              481                                                         -20M              464                                                         ______________________________________                                    

The -10 mesh slurry in the tub was allowed to settle for 72 hours andthe aqueous phase or supernatant (first wash) was siphoned off andcollected. This wash was analyzed as a slurry (solids plus solution) butwas also filtered to determine the weight of solids remaining insuspension. The settled solids were reslurried with an equal weight ofwater and were allowed to settle for 15 minutes. The supernatant secondwash) was again siphoned, collected, and analyzed. The reslurrying stepwas repeated two more times for a total of four washes. A dark slimelayer (slimes) that settled on the top of the sandy soil was left untilthe last siphoning operation when it was removed, dried, weighed andanalyzed. After the slime layer was removed, the final settled solidswere collected, dried, weighed and analyzed (-10 mesh). Typical assaysof the products from the washing cycles are reported in Table 4.

                  TABLE 4                                                         ______________________________________                                        Wet Screening and Washing of Soil                                                                                   Stream                                             Fluid    Dry Solids Percent                                                                              Assays                                  Products   (liters) (grams)    Solids ppm PCP                                 ______________________________________                                        +10M                2,280      6.9    556.4                                   -10M                27,250     83.5   135.2                                   slimes              50         0.16   567.8                                   1st wash    24.85*  12.4       0.04   13.8                                    2nd wash   22.40    2,266.9    6.9    159.0                                   3rd wash   16.90    811.2      2.5    63.0                                    4th wash    1.00    0                 10.0                                    Totals              32,640.5   100.0                                          Calculated Head                       304.6                                   ______________________________________                                         *This particular slurry was allowed to settle for 72 hours before             siphoning off the supernatant. Thus, this wash contained very few solids.

From these results it was determined that wet screening significantlyreduced the PCP content of the -10 mesh portion of the soil. A largepercentage of the PCP was found in the washes, where it was in solutionand also associated with a suspension of wood and clay material. Inaddition, it was determined that wet screening is also an effectivemeans to separate a relatively soil-free wood fraction (the +10 meshstream) containing high PCP values. The wood fraction can then bereadily incinerated.

EXPERIMENT 3 Flotation

The slurry from the wet screening operation cannot be readily filtereddue to the presence of oil and fine particles. The slimes contain asuspension of finely divided soil, small pieces of wood, and oil.Methods for the cleaning of this suspension include flotation,centrifugation, settling, and combinations thereof. Certain of theseprocesses may be undertaken in Stage 2, discussed above, and includetreatment in an attrition scrubber or pebble mill to further break upagglomerates and scrub particle surfaces before processing this slurryin a classifier to wash out fine or floatable contaminated material. Asa result of such operations, products containing relatively concentratedamounts of PCP and oil/grease components can be isolated for disposal.In particular, fine clay particles and small wood pieces are removed bythis process.

Preferably, the soil material is ultimately treated via flotation toachieve reduction of PCP concentration, or concentration of othercontaminants, to a minimum, or at least to below a desired value. Thisis a particularly effective way of obtaining a relatively clean silicasand material.

An initial evaluation of flotation with pretreatment (washing) was madeon a slurry derived from wet screening soil at 10 mesh. Slurry from ascreening operation was agitated in a flotation cell at 1200 rpm. Thesolids content of the slurry was about 10.6%. The slurry was subjectedto flotation for 15 minutes without frother addition. The cell overflowand underflow were sampled and assayed. Results are shown in Table 5.

                  TABLE 5                                                         ______________________________________                                        Flotation of a -10 Mesh Slurry from Wet Screening                                                           Product                                                                              PCP                                                 Fluid   Solids     Assay  Split                                    Product    (liters)                                                                              (grams)    ppm PCP                                                                              %                                        ______________________________________                                        froth      2.0     102.0      117.5  32.5                                     underflow  4.0     300.0      122.2  67.5                                     ______________________________________                                    

The results from this experiment indicate that flotation on materialpretreated by a single washing step generates a large overflow (froth)stream with no concentration of contaminants and handling difficultiescomparable to the feed material. However, the underflow, containingthree-fourths of the solids, responds well to settling. A conclusion isthat it is not necessarily practical to have flotation at the front endof the process flowsheet, as it does not effectively resolve the problemof slimes handling on its own. Rather, generally what is preferred,prior to flotation, is a sequential washing system to reduce the slurryhandling problem by further reducing contaminant content. This may beaccomplished through the utilization of methods as described above, forStage 2 operations. Alternatively, flotation can be used advantageouslyat the head of the flowsheet to separate intractable slimes; i.e., thefines containing a substantial amount of organics not amenable toscrubbing, for additional processing in a centrifuge or the like.

EXPERIMENT 4 Scrubbing

In a designed experimental program requiring 30 tests, the effect ofscrubbing on the removal of PCP from soil was investigated as a functionof temperature, time, pH, and concentration of surfactant. For thisexperimental design, temperature ranged from 25°-65° C., time rangedfrom 10-15 minutes, pH ranges from 5-11, and the concentration ofsurfactant ranged from 0.1-0.5 lbs./short ton of soil.

Soil contaminated with PCP was wet screened at 10 mesh to remove coarsewood. The -10 mesh fraction of the soil was slurried with water at apulp density of 50% solids. The pulp was brought to the desiredtemperature, pH was adjusted, and surfactant was added. The slurry wasscrubbed (intensely agitated) in a baffled vessel using a shroudedimpeller rotating at 1000 rpm. The pH was maintained constant throughoutthe duration of the test. At the end of the scrubbing period the slurrywas allowed to settle for 5 minutes and the aqueous phase or supernatantwas siphoned off and collected. The remaining settled solids werereslurried to 50% solids using fresh water, agitated for 15 seconds, andallowed to settle for 5 minutes before siphoning off the supernatant.The combined siphoned fluids containing a suspension of fine particleswas screened at 48 mesh to remove wood fibers. The settled solids werefiltered and the filtrate was combined with the siphoned fluids to makeup the final fluid suspension. The filtered solids and the +48 mesh woodfraction were dried overnight at 75° C. and pulverized to -100 mesh.Samples of soil, fluid, and wood were assayed for PCP.

Statistical analysis of the results showed that the level of PCPremaining in the soil is a linear function of pH and time. The leastsignificant factor was surfactant concentration regardless of whetherthe surfactant was anionic, cationic, or anionic-nonionic. The mostsignificant factor was pH. Percent removal (PR) of PCP from soil couldbe approximated by the following equation:

    PR=39.89-0.187×(minutes)-1.96×(pH)

EXPERIMENT 5 Washing Scrubbed Soils Using Classifiers

Following a flotation test such as that described in Experiment 3, thesolids remaining in the flotation apparatus exhibited a well-definedsettling pattern after the impeller stopped rotating. Invariably, ablack layer of slowly settling wood and soil formed on top of the morerapidly settling sand material. It was presumed that a classifier couldbe used to remove the lighter component, which was concluded to berather heavily contaminated with PCP.

A 3.5 inch by 2.5 foot screw classifier with a capability for bedwashing by means of bottom-bed water injection was used for thistestwork. The fee to the classifier was the -10 mesh fraction from asample of screened soil contaminated with PCP. This sample was slurriedto 50% solids with tap water and scrubbed in a mixing tank for one hourunder intense agitation. The slurry was fed to the classifier and thesand discharge and fluid overflow (first overflow) were collected. Thefluid overflow was allowed to settle and the dark layer of slimes thatsettled out on top of the fine sand was selectively removed and analyzedseparately (slimes). The remaining fluid overflow (first overflow) wasanalyzed as a slurry but also filtered to determine the weight of solidsremaining in this suspension. The sand bed in the classifier was removed(first bed), dried, weighed, and analyzed. A sample of the first sanddischarge (first product) was taken for analysis. The remaining firstsand discharge was slurried with tap water and fed back into the emptyclassifier to produce a second overflow and second sand discharge. Thesand product from the classifier was sampled for analysis (secondproduct) and recycled two more times without removing the bed tosimulate cleaning of the sand in a multi-stage system. Experimentalresults are presented in Table 6.

                  TABLE 6                                                         ______________________________________                                        Cleaning -10 Mesh Soil in a Screw Classifier                                                                PCP    PCP                                                 Fluids  Solids     Assays split                                    Stream     (liters)                                                                              (grams)    ppm PCP                                                                              %                                        ______________________________________                                        Feed               20,000     105.5                                           Products                                                                      1st Overflow                                                                             182     1,456      8.1    67.7                                     slimes             2,365      194.5  21.2                                     2nd-4th Overflow                                                                         200       400      0.1    0.9                                      1st Bed            3,630      31.2   5.2                                      1st Product          124      8.4                                             2nd Product          122      7.2    0.2                                      3rd Product          126      7.5                                             Final Bed          2,000      8.0    0.7                                      Final Product      10,831     8.1    4.1                                                         21,056     103.1  100.0                                    ______________________________________                                    

The above data support the conclusion that a substantial amount of PCPremoval can be accomplished through utilization of a classifier, priorto introduction of the soil material into a flotation cell or the like.However, at some point during recycling of classified sands, no furthersubstantial PCP removal was observed. This suggests that the PCPremaining in the classifier sand product is locked in particles of sizeand density comparable to the sand particulates. Release of PCP fromthese particles could be facilitated through the use of a rigorousscrubbing stage or attrition stage prior to additional stages ofclassification, as illustrated in Experiment 6. Alternatively, the bulkof the remaining portion of the PCP and oil/grease material can beremoved in a flotation cell, as illustrated in Experiment 7.

EXPERIMENT 6 Washing Soils Using Multi-Stage Classification withInterstage Scrubbing

This test, following the procedures established in Experiment 5, wasdesigned to better simulate a bank of classifiers by removing the bed inthe laboratory screw classifier prior to recycling the sand dischargeproduct back into the same classifier to simulate the next state. Also,interstage scrubbing was simulated by scrubbing the classifier sanddischarge product in a flotation cell at 2100 rpm. Thus, a -10 mesh soilsample contaminated with PCP was slurried with tap water to 50% solids,scrubbed in a flotation cell, and fed to the screw classifier.Classifier overflow (first slurry) and sand discharge were collected.The sand bed remaining in the classifier (first bed) was removed, dried,weighed and analyzed. A sample of sand discharge was taken for analysis(first sand) and the remaining sand product was slurried with tap water,subjected to attrition scrubbing in a flotation cell for 15 minutes at2100 rpm, and fed back into the empty classifier for the second stage ofwashing. This cycle was repeated twice for a total of three stages ofcleaning. Results are presented in Table 7. this data indicates thatwith proper intensity of interstage scrubbing the soil can be cleanedfrom 120 ppm PCP to approximately 5-10 ppm PCP in two to three stages.

                  TABLE 7                                                         ______________________________________                                        Cleaning Soil by Multistage Classification                                    with Interstage Scrubbing                                                                                   Stream PCP                                                  Fluid   Solids    Assay  split                                    Stream      (liters)                                                                              (grams)   ppm PCP                                                                              %                                        ______________________________________                                        Feed                12,000    120                                             Products                                                                      1st Slurry  83        916.3   14.9   86.1                                     1st Bed             2,080.0   49.6   7.2                                      1st Sand              65.2    8.2    0.0                                      2nd Slurry  76        113.6   0.3    1.4                                      2nd Bed             2,155.0   12.8   1.9                                      2nd Sand              56.8    9.1    0.0                                      Final Slurry                                                                              45        22.7    0.2    0.6                                      Final Bed           1,520.0   7.1    0.8                                      Final Sand          4,550.0   6.3    2.0                                      Calculated Feed Assay 125.3                                                   ______________________________________                                    

EXPERIMENT 7 Soil Polishing by Flotation

As previously described, final removal of PCP from the soil, i.e., apolishing step, can be accomplished through flotation. This unique stepleads to a final soil product which is very low in PCP, and which can bedisposed of in manners not necessarily requiring special handling indump sites.

A soil contaminated with PCP was processed through five stages ofscrubbing at a pH of 9.5 to prepare a scrubbed soil slurry as feed forflotation tests. The slurry was adjusted to 33% solids and was floatedfor 5 minutes. It was then conditioned with 0.3 lbs. pine oil orMIBC/short ton of soil and floated for another 10 minutes. Additionaltests were performed in which two stages of flotation were conducted byconditioning for 10 minutes with 0.1 lbs. pine oil/short ton of soil andpulling froth for 5 minutes. The combined froth products, underflowsolids, and underflow filtrate were analyzed for PCP. Typical resultsare given in Table 8 below.

                  TABLE 8                                                         ______________________________________                                        Polishing Scrubbed Soil by Flotation                                                                               PCP                                                Fluid   Solids             split                                    Stream    (liters)                                                                              (grams)     PCP ppm                                                                              %                                        ______________________________________                                        Feed              500         9.2                                             Froth     0.4     1.8         2.3    18.8                                     Underflow                                                                     Solids            494.5       4.6    47.0                                     Filtrate  1.4                 1.2    34.2                                     Calculated Feed Assay 9.6                                                     ______________________________________                                    

From the above data, which were consistent for all tests, it can beconcluded that the polishing operation may be used to reduce the PCPcontent of the final soil by as much as 50%. The solid material in thefroth appeared to be mostly clay. The sand material was released in arelatively clean form. Results also indicated that it appears beneficialto operate at a basicity within the pH range of 7-8.

EXPERIMENT 8 Empirical Data Supporting the Assertion of AttritionScrubbing

A soil particle size analysis with associated pentachlorophenol (PCP)levels of each size fraction, of soil entering and exiting a 500 lb. perhour continuous pilot plan are provided below in Table 9. In the pilotsystem, the soil was subjected to wet screening, froth flotation, andattrition scrubbing/classification operation as generally abovedescribed. Coarse, woody debris and highly contaminated fine particleswere removed from the soil, altering the overall size distribution. Sizeanalysis was determined by wet sieving at 400 mesh, following by drysieving of the +400 mesh material on 20-400 mesh sieves.

Comparison of PCP levels in the feed and washed soil illustrates theeffect of a multi-stage attrition/classification circuit as outlined inthe detailed description above. In addition, the relatively high PCPlevel in the small amount of -400 mesh material remaining in the washedsoil, shows where the desired particle size split was to have been madein the classification step. That is, there is relatively little PCPcontamination in the washed soil resulting from fractions at about 150mesh to 400 mesh, since the weight percent of material in washed soil isrelatively small from these fractions and the PCP concentration fromthese fractions was also relatively small. However, at about 400 mesh orbelow, the PCP concentration present rises considerably. That is,material at about 400 mesh or below should be minimized, to the extentreasonable, in the "cleansed" material.

It will be readily understood that an analysis such as described above,and represented in Table 9, indicates how a determination can be made onwhere a "cut" is to be taken for defining a "cleansed" fraction. Ingeneral, it is a matter of determining how much contamination resultsfrom each fraction, and adjusting the classification system accordingly.The determination is in part made by balance of the acceptability ofsome contamination to the final "cleansed" material vs. the cost ofhandling more solids in the waste water stream. The level ofcontamination acceptable in the final "cleansed" fraction will usuallybe set by local ordinance, regulations or specific need.

                  TABLE 9                                                         ______________________________________                                        Soil Particle Size Analysis                                                   Tyler         Feed Soil        Washed Soil                                    Mesh          Weight   PCP     Weight PCP                                     Size          Percent  (ppm)   Percent                                                                              (ppm)                                   ______________________________________                                        +20           3.9      712     1.0    24.8                                    -20 +35       39.9     512     8.7    19.2                                    -35 +65       29.8     341     37.1   11.0                                    -65 +150      21.7     343     44.5   12.9                                    -150 +270     3.8      614     8.3    20.7                                    -270 +400     .3       995     0.3    34.8                                    -400          0.6      904     0.1    103.0                                   ______________________________________                                    

It is to be understood that while certain embodiments of the presentinvention have been illustrated and described, the invention is not tobe limited to the specific steps, forms or arrangements herein describedand shown, except as limited by the following claims.

What is claimed and desired to be secured by patent:
 1. A process fortreating soil contaminated with organic materials; said processincluding the steps of:(a) forming a slurry of less than about 10 meshcontaminated soil material in a fluid; said contaminated soil slurrycontaining 40-70% solids by weight; (b) conducting an attrition processon the contaminated soil slurry to break the soil into particles andgenerate in fluid suspension sufficient particle/particle collisions toabrade contaminant off larger particles; and (c) conducting aclassification process on the fluid suspension of particles from saidattrition process, for isolation and removal of a fraction containingrelatively fine, slow settling, particles of less than about 10 micronsin size, from a fraction containing coarser, faster settling, particles,by means of relative settling velocities; said step of classificationbeing performed prior to complete settling of the suspension formed insaid attrition process.
 2. The process according to claim 1 wherein:(a)said steps of forming a slurry, conducting an attrition process andconducting a classification process involve the use of a countercurrentflow of the soil and the fluid; and (b) said step of classificationinvolves substantial removal of a relatively fine particle soil organiccomponent from said soil, as part of the fraction containing slowsettling particles.
 3. The process according to claim 1 wherein saidstep of forming a slurry of less than about 10 mesh soil materialincludes forming a slurry of soil material containing less than about50% of the particles having a size smaller than about 200 mesh.
 4. Theprocess according to claim 3 wherein said step of forming a slurry ofless than about 10 mesh soil material includes forming a slurry of soilmaterial containing less than about 30% of the particles having a sizesmaller than about 200 mesh.
 5. The process according to claim 1including a step of subjecting the contaminated soil slurry to aflotation treatment involving floating particles of the soil in aflotation cell in the presence of microbubbles of air in a sufficientconcentration to encounter said particles and selectively partitionhydrophobic materials including organics in said soil to an interfacewith said bubbles; whereby said organic materials may be floated to anupper surface of said flotation cell.
 6. The process according to claim5 wherein said organics include oil with pentachlorophenol dissolvedtherein.
 7. The process according to claim 1 wherein:(a) said step ofconducting an attrition process on the contaminated soil slurry involvesthe use of an attrition cell capable of generating abrasive action; and(b) said step of classification involves the use of a countercurrentflow of the soil and the fluid.
 8. A process for treating soilcontaminated with organic material; said process including the stepsof:(a) extracting said soil from the environment and screening same toform a screen undersized material having a size generally less thanabout 10 mesh; (b) forming a slurry of the screen undersized material ina fluid, the slurry containing 40-70% solids by weight; said solidscontaining less than about 50% of the particles with a size smaller thanabout 200 mesh; (c) subjecting the screen undersized material slurry toan attrition process using an attrition device to break the materialinto particles and generate in fluid suspension sufficientparticle/particle collisions to abrade contaminant off larger particles;and (d) conducting a classification process on the suspension ofparticles from said attrition process, for isolation and removal of afraction containing relatively fine, slow settling particles having asize less than about 74 microns in size, from a fraction containinglarger, faster settling particles, on the basis of relative settlingvelocities; said step of classification being performed prior tocomplete settling of the suspension of particles from said attritionstep.
 9. The process according to claim 8 including a step of conductinga flotation step at some point prior to conducting the classificationprocess; said step of flotation including floating soil material in aflotation cell in the presence of microbubbles of air in sufficientconcentration to encounter said soil material and selectively partitionhydrophobic materials including organics in said soil to an interfacewith said bubbles; whereby said organics are separated from said soilmaterial and are floated to an upper portion of said flotation cell. 10.The process according to claim 8 wherein:(a) said step of classificationinvolves passage of the screen undersized material into a classifiersystem with a countercurrent flow of material; (b) whereby a fractioncontaining small wood materials and relatively fine, contaminated soilmaterials are selectively removed from said soil; said fractioncontaining wood and relatively fine, contaminated soil materialsgenerally including a disproportionate amount of contaminates therein.11. The process according to claim 10 wherein said classifier systemincludes a plurality of screw classifiers arranged in series.
 12. Theprocess according to claim 8 wherein:(a) said step of classificationinvolves passage of the screen undersized material into a cyclone systemwith a countercurrent flow of material; (b) whereby a fractioncontaining small wood materials and relatively fine, contaminated soilmaterials are selectively removed from said soil; said fractioncontaining wood and relatively fine, contaminated soil materialsgenerally including a disproportionate amount of contaminants therein.13. The process according to claim 8 further including:(a) subjectingsaid faster settling particles from said classification process to asecond attrition process to form a second suspension; and (b) subjectingsaid second suspension to a second classification process.
 14. Theprocess according to claim 8 wherein said steps of forming a slurry,subjecting the slurry to an attrition process, and conducting aclassification process on the slurry are performed under conditions of acountercurrent flow of the soil and the fluid.
 15. A process fortreating soil contaminated with organic material; said process includingthe steps of:(a) excavating said soil from a site and classifying thesame to remove bulk items therefrom by passage through a grizzly; (b)breaking said soil into smaller particles by means of a trommel; (c)screening said smaller particles to less than about 10 mesh; (d) forminga slurry of the -10 mesh material in a fluid; (e) subjecting the -10mesh material to a first attrition process to break the material intoparticles and generate in fluid suspension sufficient particle/particlecollisions to abrade contaminant off larger particles; (f) conducting afirst classification process on the suspension of particles from saidfirst attrition process, for isolation and removal of a fractioncontaining relatively fine, slow settling particles having a size ofless than about 10 microns from a fraction containing faster settlingparticles; (g) subjecting the fraction of the particle suspensioncontaining the faster settling particles to a second attrition processto form a second suspension of particles in fluid; (h) conducting asecond classification process on the second suspension of particles forfurther isolation and removal of a fraction containing particles havinga size less than about 10 microns; and (i) performing said steps offorming a slurry, subjecting the slurry to an attrition process, andconducting a classification process on the slurry under conditions of acountercurrent flow of the soil and the fluid.
 16. The process accordingto claim 15 wherein the step of forming a slurry of the -10 meshmaterial in a fluid involves forming a slurry containing 40-70% solidsby weight.
 17. The process according to claim 16 wherein said solids insaid slurry contain less than about 50% of the particles with a sizesmaller than about 200 mesh.
 18. The process according to claim 15wherein said process includes a plurality of attrition andclassification steps.
 19. The process according to claim 15 wherein saidstep of forming a slurry includes forming a slurry of the -10 meshmaterial in water.